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Integrated Continuous Processing and Flow Characterization of RAFT Polymerization in Tubular Flow Reactors

机译:管状流反应器中RAFT聚合反应的集成连续过程和流动特性

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摘要

Several unit operations are combined in series to form an integrated, continuous polymerization process; namely inline degassing of monomer stock solution prior to reaction, polymerization using the RAFT approach and precipitation after reaction to form a solid polymeric product. The polymerization is conducted at 70-80℃ with reaction times of 30-90 min in a stainless steel tubular flow reactor, yielding poly(acrylamide) at high conversion (typically >90%) and with a low polydispersity of 1.14-1.23. The axial dispersion occurring inside the tubular flow reactor during polymerization is characterized by reaction profiling using a series of NMR samples. The process can be scaled up to a total output of 1.36 kg of polymer per day on this laboratory-scale reactor.
机译:几个单元操作串联在一起以形成一个集成的连续聚合过程。即在反应之前将单体储备溶液进行在线脱气,使用RAFT方法进行聚合,以及在反应之后进行沉淀以形成固体聚合物。在不锈钢管式流动反应器中,聚合反应在70-80℃,反应时间为30-90分钟的条件下进行,以高转化率(通常> 90%)和低多分散度(1.14-1.23)得到聚丙烯酰胺。聚合过程中发生在管式流动反应器内部的轴向分散的特征是使用一系列NMR样品进行反应分析。在该实验室规模的反应器上,该工艺可以按比例放大至每天总产量1.36 kg聚合物。

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  • 来源
    《Macromolecular reaction engineering》 |2012年第11期|p.458-466|共9页
  • 作者单位

    CSIRO Materials Science and Engineering, Bag 10, Clayton South, Victoria 3169, Australia;

    CSIRO Materials Science and Engineering, Bag 10, Clayton South, Victoria 3169, Australia;

    CSIRO Materials Science and Engineering, Bag 10, Clayton South, Victoria 3169, Australia;

    CSIRO Materials Science and Engineering, Bag 10, Clayton South, Victoria 3169, Australia;

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